Movatterモバイル変換


[0]ホーム

URL:


US4622259A - Nonwoven medical fabric - Google Patents

Nonwoven medical fabric
Download PDF

Info

Publication number
US4622259A
US4622259AUS06/763,508US76350885AUS4622259AUS 4622259 AUS4622259 AUS 4622259AUS 76350885 AUS76350885 AUS 76350885AUS 4622259 AUS4622259 AUS 4622259A
Authority
US
United States
Prior art keywords
fabric
fibers
strength
fabrics
web
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US06/763,508
Inventor
Larry H. McAmish
Tralance O. Addy
George F. Lee
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ethicon Inc
JPMorgan Chase Bank NA
Original Assignee
Surgikos Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Surgikos IncfiledCriticalSurgikos Inc
Assigned to SURGIKOS, INC., A CORP OF NEW JERSEYreassignmentSURGIKOS, INC., A CORP OF NEW JERSEYASSIGNMENT OF ASSIGNORS INTEREST.Assignors: ADDY, TRALANCE O., MC AMISH, LARRY H., LEE, GEORGE F.
Priority to US06/763,508priorityCriticalpatent/US4622259A/en
Priority to US06/884,563prioritypatent/US4908163A/en
Priority to NZ216982Aprioritypatent/NZ216982A/en
Priority to CA000515440Aprioritypatent/CA1318993C/en
Priority to AU60941/86Aprioritypatent/AU592811B2/en
Priority to DE8686111123Tprioritypatent/DE3687053T2/en
Priority to BR8603783Aprioritypatent/BR8603783A/en
Priority to JP61184343Aprioritypatent/JPS6245763A/en
Priority to ZA865951Aprioritypatent/ZA865951B/en
Priority to ES8600929Aprioritypatent/ES2001071A6/en
Priority to EP86111123Aprioritypatent/EP0212540B1/en
Publication of US4622259ApublicationCriticalpatent/US4622259A/en
Application grantedgrantedCritical
Assigned to JOHNSON & JOHNSON MEDICAL, INC., A NJ CORP.reassignmentJOHNSON & JOHNSON MEDICAL, INC., A NJ CORP.MERGER (SEE DOCUMENT FOR DETAILS).Assignors: JOHNSON & JOHNSON PATIENT CARE, INC., STERILE DESIGN, INC., (MERGED INTO), SURGIKOS, INC. (CHANGED TO)
Assigned to CHICOPEE, INC.reassignmentCHICOPEE, INC.ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS).Assignors: JOHNSON & JOHNSON MEDICAL, INC.
Assigned to CHASE MANHATTAN BANK, THE, (N.A.)reassignmentCHASE MANHATTAN BANK, THE, (N.A.)SECURITY INTEREST (SEE DOCUMENT FOR DETAILS).Assignors: CHICOPEE, INC.
Assigned to CHASE MANHATTAN BANK, THE, (THE)reassignmentCHASE MANHATTAN BANK, THE, (THE)CORRECTIVE ASSIGNMENT TO CORRECT EXECUTION DATE.Assignors: CHICOPEE, INC.
Assigned to CHASE MANHATTAN BANK (NATIONAL ASSOCIATION)reassignmentCHASE MANHATTAN BANK (NATIONAL ASSOCIATION)SECURITY INTEREST (SEE DOCUMENT FOR DETAILS).Assignors: CHICOPEE, INC., FIBERTECH GROUP, INC., POLYMER GROUP, INC.
Assigned to CHASE MANHATTAN BANK, THEreassignmentCHASE MANHATTAN BANK, THESECURITY INTEREST (SEE DOCUMENT FOR DETAILS).Assignors: CHICOPEE, INC.
Assigned to JPMORGAN CHASE BANKreassignmentJPMORGAN CHASE BANKSECURITY AGREEMENTAssignors: CHICOPEE, INC.
Assigned to CHICOPEE, INC.reassignmentCHICOPEE, INC.RELEASE OF SECURITY INTERESTAssignors: JPMORGAN CHASE BANK, AS ADMINISTRATIVE AGENT
Assigned to CITICORP NORTH AMERICA, INC. AS FIRST LIEN COLLATERAL AGENTreassignmentCITICORP NORTH AMERICA, INC. AS FIRST LIEN COLLATERAL AGENTSECURITY AGREEMENTAssignors: CHICOPEE, INC., FIBERTECH GROUP, INC, POLY-BOND, INC., POLYMER GROUP, INC.
Assigned to WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENTreassignmentWILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENTSECURITY AGREEMENTAssignors: CHICOPEE, INC., FIBERTECH GROUP, INC., POLY-BOND, INC., POLYMER GROUP, INC.
Anticipated expirationlegal-statusCritical
Assigned to FNA POLYMER CORP., PGI EUROPE, INC., BONLAM (S.C.), INC., PRISTINE BRANDS CORPORATION, FABRENE GROUP L.L.C., POLY-BOND INC., TECHNETICS GROUP, INC., FIBERTECH GROUP, INC., CHICOPEE, INC., LORETEX CORPORATION, POLYLONIX SEPARATION TECHNOLOGIES, INC., FIBERGOL CORPORATION, FABRENE CORP., PGI POLYMER, INC., DOMINION TEXTILE (USA) INC., POLYMER GROUP, INC., FNA ACQUISITION, INC., PNA CORPORATION, FABPRO ORIENTED POLYMERS, INC.reassignmentFNA POLYMER CORP.RELEASE OF SECURITY INTEREST IN PATENTSAssignors: CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT
Assigned to PGI EUROPE, INC., FABPRO ORIENTED POLYMERS, INC., POLYMER GROUP, INC., LORETEX CORPORATION, FABRENE GROUP L.L.C., FNA ACQUISITION, INC., FNA POLYMER CORP., FABRENE CORP., PGI POLYMER, INC., BONLAM (S.C.), INC., FIBERGOL CORPORATION, PRISTINE BRANDS CORPORATION, TECHNETICS GROUP, INC., PNA CORPORATION, DOMINION TEXTILE (USA) INC., POLYLONIX SEPARATION TECHNOLOGIES, INC., POLY-BOND INC., CHICOPEE, INC., FIBERTECH GROUP, INC.reassignmentPGI EUROPE, INC.RELEASE OF SECURITY INTEREST IN PATENTSAssignors: WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT
Expired - Lifetimelegal-statusCriticalCurrent

Links

Images

Classifications

Definitions

Landscapes

Abstract

A nonreinforced microfiber fabric is disclosed. The fabric has minimum grab tensile strength to weight ratio greater than 0.8N per gram per square meter and a minimum Elmendorf tear strength to weight ratio greater than 0.04N per gram per square meter. The fibers in the fabric have an average length greater than 10 centimeters and at least 80% of the fibers have a diameter of 7 microns or less. The fabric is made by thermally embossing a microfiber web which is made with a minimum of degradation to the polymer and employing high velocity secondary air to maintain air flow uniformity and fiber length.

Description

FIELD OF THE INVENTION
The present invention relates to nonwoven fabrics made of unreinforced microfiber webs, characterized by high strength, and especially suitable for use as medical fabrics.
BACKGROUND OF THE INVENTION
The present invention is directed to nonwoven fabrics and particularly to medical fabrics. The term "medical fabric", as used herein, is a fabric which may be used as the fabric for surgical drapes, surgical gowns, instrument wraps, or the like. Such medical fabrics have certain required properties to insure that they will perform properly for the intended use. These properties include strength, the capability of resisting water or other liquid penetration, often referred to as strike-through resistance, as well as being breathable, soft, drapable, sterilizable and a bacterial barrier.
In important areas, some of these characteristics or attributes appear to be in direct opposition in one another in a given fabric, and consequently, conventional disposable medical fabrics have not achieved an optimum balance of the desired attributes. For instance, with prior art fabrics which are comprised predominantly of spunbonded webs, random-laid staple fiber webs, tissue and scrim laminates, spunlaced webs, or combinations thereof, attempts to improve the key repellency or barrier properties invariably compromise breathability and softness attributes. Thus, those fabrics with superior breathability and other aesthetic attributes tend to be relatively inferior in strike-through resistance. As a further example, in order to improve strength, it is generally known to increase the weight of the fabric, compact the web to a high degree, add or increase binders, or adopt various combinations of these techniques. However, such attempts often result in undesirable aesthetic characteristics, as the resulting fabrics tend to be generally stiffer and less breathable.
The use of microfiber webs in applications where barrier properties are desired is known in the prior art. Microfibers are fibers having a diameter of from less than 1 micron to about 10 microns. Microfiber webs are often referred to as melt-blown webs as they are usually made by a melt blowing process. It is generally recognized that the use of relatively small diameter fibers in a fabric structure should allow the achievement of high repellency or filtration properties without undue compromise of breathability. Microfiber web fabrics made heretofore, and intended for use as medical fabrics, have been composites of microfiber webs laminated or otherwise bonded to spunbonded thermoplastic fiber webs, or films, or other reinforcing webs which provide the requisite strength to the fabric. The microfiber, melt-blown webs heretofore developed have been reported to possess insufficient strength, when unreinforced, to be used in medical or other applications where high strength at relatively low weights is desirable or important. For example, in the "Journal of Industrial Fabrics", Vol. 3, No. 1, 1984, pages 33-44, it is indicated that the most serious deficiency of melt-blown webs is their strength per unit weight when compared to conventional webs or scrims of the same material. Japanese Patent Application Disclosure 180, 653-1983 indicates that melt-blown sheets lack tensile strength and attributes this deficiency to the fact that the melt-blown sheets are formed of undrawn fibers. United Kingdom Patent Application Disclosure G.B. No. 2104562A, discloses that other fibrous reinforcements are necessary to impart strength to melt-blown webs for use as medical fabrics. U.S. Pat. No. 4,041,203 discloses a nonwoven fabric made by combining microfiber webs and spunbonded webs to produce a fabric useful as a medical fabric. The patent gives various examples demonstrating the necessity of reinforcing melt-blown webs to provide adequate strength. Example 1 of the patent describes a thermally point-bonded melt-blown web before and after addition of a spunbonded reinforcement layer. The grab tensile strength to basis weight ratio of the embossed unreinforced melt-blow web was lower than can be used for medical fabrics at practical weight levels. The patent further specifically discloses various webs made with polypropylene. The microfiber webs and the continuous-filament, polypropylene, spunbonded webs are laminated together through the application of heat and pressure in a pattern to produce a medical fabric. The continuous-filament, spunbonded web provides the strength to the laminated fabric.
U.S. Pat. No. 4,302,495 discloses a laminate of a microfiber web and a directionally-oriented thermoplastic netting. The thermoplastic netting provides the requisite strength to the finished nonwoven fabric.
U.S. Pat. No. 4,196,245 discloses combinations of melt-blown or microfine fibers with apertured films or with apertured films and spunbonded fabrics. Again, the apertured film and the spunbonded fabric are the components in the finished, nonwoven fabric which provide the strength to the fabric.
While the above-mentioned fabrics have the potential to achieve a better balance of repellency and breathability compared to other prior art technologies not using microfibers, the addition of reinforcement layers of relatively large diameter fibers limits their advantages. The fabrics have to be assembled using two or more web forming technologies, resulting in increased process complexity and cost. Furthermore, the bonding of relatively conventional fibrous webs to the microfibers can result in stiff fabrics, especially where high strength is desired.
BRIEF SUMMARY OF THE INVENTION
The present invention seeks to avoid the limitations of the above-mentioned prior art fabrics by providing a medical fabric from an unreinforced web or webs of microfine fibers. The present fabric is unreinforced in that it need not be laminated or bonded to another type of web or film to provide adequate strength to be used in medical applications. The fabric of the present invention also achieves a balance of repellency, strength, breathability and other aesthetics superior to prior art fabrics.
The requirements for medical grade fabrics are quite demanding. The fabric must have sufficient strength to resist tearing or pulling apart during normal use, for instance, in an operating room environment. This is especially true for fabrics that are to be used for operating room apparel such as surgical gowns or scrub suits or for surgical drapes. One measure of the strength of a nonwoven fabric is the grab tensile strength. The grab tensile strength is generally the load necessary to pull apart or break a 10 cm wide sample of the fabric.
The test for grab tensile strength of nonwoven fabrics is described in ASTM D1117. Nonwoven medical fabrics must also be resistant to tearing. The tearing strength or resistance is generally measured by the Elmendorf Tear Test as described in ASTM D1117. As an example, the grab tensile strengths, measured in the weakest, normally cross machine direction, of the least strong commercially used medical fabrics are in the range of 45 newtons (N) with tear strengths in the weakest direction of approximately 2 N. At these levels of strength, fabric failure can often occur in fabrics during use as gowns and drapes, and it is generally desired to achieve higher strength levels. Grab tensile strength levels of approximately 65 N and above and tear resistance levels of approximately 6 N and above would allow a particular medical fabric to be used in a wider range of applications. It is an objective of the present invention to provide a fabric with high strength to weight ratio, such that at desirable weights, both grab tensile and tear strengths higher than the above values can be achieved. The fabrics of the present invention generally have basic weights in the range of 14 to 85 g/m2.
Medical fabrics must also be repellent to fluids including blood, that are commonly encountered in hospital operating rooms. Since these fluids offer a convenient vehicle for microorganisms to be transported from one location to another, repellency is a critical functional attribute of medical fabrics. A measure of repellency that is influenced primarily by the pore structure of a fabric is the "hydrostatic head" test, AATCC 127-1977. The hydrostatic head test measures the pressure, in units of height of a column of water, necessary to penetrate a given sample of fabric. Since the ultimate resistance of a given fabric to liquid penetration is governed by the pore structure of the fabric, the hydrostatic head test is an effective method to assess the inherent repellent attributes of a medical fabric. Nonwoven medical fabrics which do not include impermeable films or microfiber webs generally possess hydrostatic head values between 20 to 30 cm of water. It is generally recognized that these values are not optimum for gowns and drapes, especially for those situations in which the risk of infection is high. Values of 40 cm or greater are desirable. Unfortunately, prior art disposable fabrics which possess high hydrostatic head values are associated with low breathability or relatively low strength. It is another objective of the present invention to provide a fabric which can attain a high level of fluid repellency.
The breathability of medical fabrics is also a desirable property. This is especially true if the fabrics are to be used for wearing apparel. The breathability of fabrics is related to both the rate of moisture vapor transmission (MVTR) and air permeability. Since most fibrous webs used for medical fabrics possess reasonably high levels of MVTR, the measurement of air permeability is an appropriate discriminating quantitative test of breathability. Generally the more open the structure of a fabric, the higher its air permeability. Thus, highly compacted, dense webs with very small pore structures result in fabrics with poor air permeability and are consequently perceived to have poor breathability. An increase in the weight of a given fabric would also decrease its air permeability. A measure of air permeability is the Frazier air porosity test, ASTM D737. Medical garments made of fabrics with Frazier air porosity below 8 cubic meters per minute per square meter of fabric would tend to be uncomfortable when worn for any length of time. It is a further objective of the present invention to provide a fabric which achieves good breathability without sacrifice of repellency or strength.
Medical fabrics must also have good drapability, which may be measured by various methods including the Cusick drape test. In the Cusick drape test, a circular fabric sample is held concentrically between horizontal discs which are smaller than the fabric sample. The fabric is allowed to drape into folds around the lower of the discs. The shadow of the draped sample is projected onto an annular ring of paper of the same size as the unsupported portion of the fabric sample. The outline of the shadow is traced onto the annular ring of paper. The mass of the annular ring of paper is determined. The paper is then cut along the trace of the shadow, and the mass of the inner portion of the ring which represents the shadow is determined. The drape coefficient is the mass of the inner ring divided by the mass of the annular ring times 100. The lower the drape coefficient, the more drapable the fabric. Drapability correlates well with softness and flexibility.
In addition to the above characteristics, medical grade fabrics must have anti-static properties and fire retardancy. The fabrics should also possess good resistance to abrasion, and not shed small fibrous particles, generally referred to as lint.
The present invention provides a melt blown or microfiber fabric which has adequate strength and tear resistance, without reinforcement, to be used as a medical fabric and in other applications where high strength and tear resistance are required. The embossed fabrics of the present invention have a minimum grab tensile strength to weight ratio of at least 0.8 N per gram per square meter and a minimum Elmendorf tear strength to weight ratio of at least 0.04 N per gram per square meter. These strength properties are achieved while also obtaining the properties of repellency, air permeability and drapability that are desired for the use of the fabric in medical applications.
In addition to the strength characteristics mentioned above, the fabric of the present invention differs from prior art melt blown webs in that the average length of the individual fibers in the web is greater than the average length of the fibers in prior art webs. The average fiber length in the present webs is greater than 10 cm, preferrably greater than 20 cm and most preferably in the range of 25 to 50 cm. Also, the average diameter of the fibers in the web should be no greater than 7 microns. The distribution of the fiber diameters is such that at least 80% of the fibers have a diameter no greater than 7 microns and preferrably at least 90% of the fibers have a diameter no greater than 7 microns.
In the description of the present invention the term "web" refers to the unbonded web formed by the melt blowing process. The term "fabric" refers to the web after it is bonded by heat embossing or other means.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is an isometric view of the melt-blowing process.
FIG. 2 is a cross-sectional view of the placement of the die and the placement of the secondary air source.
FIG. 3 is a detailed fragmentary view of the extrusion die illustrating negative set back.
FIG. 4 is a detailed fragmentary view of the extrusion die illustrating positive set back.
FIG. 5 is a graph comparing the effects of gauge length on the strip tensile strength of two samples of unembossed webs.
FIG. 6 is similar to FIG. 5 except that the plot is for point-bonded thermally embossed fabrics of the webs of FIG. 5.
DETAILED DESCRIPTION OF THE INVENTION
As shown in FIG. 1, the process of the present invention is carried out in conventional melt-blowing equipment which has been modified to provide high velocity secondary air. In the apparatus shown, a thermoplastic resin in the form of pellets or granules, is fed into ahopper 10. The pellets are then introduced into the extruder 11 in which the temperature is controlled through multiple heating zones to raise the temperature of the resin above its melting point. The extruder is driven by amotor 12 which moves the resin through the heating zones of the extruder and into thedie 13. The die 13 may also have multiple heating zones. The resin passes from the extruder into aheater chamber 29 which is between the upper and lower dieplates 30 and 31. The upper and lower die plates are heated byheaters 20 to raise the temperature of die and the resin in thechamber 29 to the desired level. The resin is then forced through a plurality ofminute orifices 17 in the face of the die. Conventionally, there are about 12 orifices per centimeter of width of the die. An inert hot gas, usually air, is forced into the die throughlines 14 intogas chamber 19. The heated gas, known as primary air, then flows togas slots 32 and 33 which are located in either side of theresin orifices 17. The hot gas attenuates the resin into fibers as the resin passes out of theorifices 17. The width of theslot 32 or 33 is referred to as the air gap. The fibers are direced by the hot gas onto a web formingforaminous conveyor 22 to form a mat orweb 26. It is usual to employ avacuum box 23 attached to asuitable vacuum line 24 to assist in the collection of the fibers. Thescreen 22 is driven aroundrollers 25 so as to form a web continuously. In the present process, the fibers are contacted by high velocity secondary air immediately after the fibers exit the die. The secondary air is ambient air at room temperature or at outside air temperature. If desired, the secondary air can be chilled. The secondary air is forced under pressure from an appropriate source throughfeed lines 15 and intodistributor 16 located on each side of the die. The distributors are generally as long as the face of the die. The distributors have an angledface 35 with anopening 27 adjacent the die face. The velocity of the secondary air can be controlled by increasing the pressure infeed line 15 or by the use of abaffle 28. The baffle would restrict the size of theopening 27, thereby increasing the velocity of air exiting the distribution box, at constant volume. The outlets of theorifices 17 and thegas slots 32 and 33 may be in the same plane or may be offset. FIG. 3 shows theorifice 17 terminating inward of the face of the die and theslots 32 and 33. This arrangement is referred to as negative setback. The setback dimension is shown by the space between the arrows in FIG. 3. Positive setback is illustrated in FIG. 4. The outlet of theorifice 17 terminates outward of the face of the die and theslots 32 and 33. The setback dimension is shown by the space between the arrows in FIG. 4. A negative setback is preferred in the present process as it allows greater flexibility in setting the air gap without adversely effecting the quality of the web produced.
The present nonwoven fabric differs from prior art microfiber-containing fabrics in the utilization of the melt-blowing process to produce microfibers with characteristics which result in uniquely high fabric strength to weight ratios, if the fibers are formed into a web and thermally bonded as described herein.
In the practice of prior art melt-blown technology for fabric related applications, it is typical to produce microfibers which range in average diameter from about 1 to 10 microns. While in a given web, there may be a range of fiber diameters, it is often necessary to keep the diameters of these fibers low in order to fully exploit the advantages of microfiber structures as good filtration media. Thus, it is usual to produce webs or batts with average fiber diameters of less than 5 microns or at times even less than 2 microns. In such prior art processes, it is also typical for such fibers to be of average lengths between 5 to 10 centimeters (cm). As discussed in the review of the prior art fabrics, the webs formed from such fibers have very low strength. The tensile strength of such a web is primarily due to the bonding that occurs between fibers as they are deposited on the forming conveyor. Some degree of interfiber surface bonding can occur because in the conventional practice of melt-blown technology, the fibers may be deposited on the forming conveyor in a state in which the fibers are not completely solid. Their semi-molten surfaces can then fuse together at cross-over points. This bond formation is sometimes referred to as autogenous bonding. The higher the level of autogenous bonding, the higher the integrity of the web. However, if autogenous bonding of the thermoplastic fibers is excessively high, the webs become stiff, harsh and quite brittle. The strength of such unembossed webs is furthermore not adequate for practical applications such as medical fabrics. Thermal bonding of these webs can generally improve strength. However, as discussed in previous sections, without introduction of substantial amounts of reinforcing elements such as other types of fibers, binders, etc., it has heretofore not been possible to produce melt-blown microdenier fabrics with high strength, particularly for use as surgical gowns, scrub apparel and drapes, where tensile and tear strengths are important.
In forming the webs of the fabric of the present invention, fibers are produced which are longer than fibers of the prior art. Fiber lengths were determined using rectangular-shaped wire forms. These forms had span lengths ranging from 5 to 50 cm in 5 cm increments. Strips of double-faced adhesive tape were applied to the wire to provide adhesive sites to collect fibers from the fiber stream. Fiber lengths were determined by first passing each wire form quickly through the fiber stream, perpendicular to the direction of flow, and at a distance closer to the location of the forming conveyor than to the melt blowing die. Average fiber lengths were then approximated on the basis of the number of individual fibers spanning the wire forms at successive span lengths. Applicants have discovered that if a substantial portion of the fibers are longer than 10 cm, such that the average fiber length is at least greater than 10 cm and preferably greater than 20 cm, the webs, thus formed, can result in embossed fabrics with unique strength, while maintaining other desired features of a medical fabric. Fabrics with highly desirable properties are produced when average fiber lengths are in the range of 25 to 50 cm. In order to maintain the potential of microdenier fibers to resist liquid penetration, it is necessary to keep the diameters of the fibers low. In order to develop high repellency, it is necessary for the average diameter of the fibers of the present fabric to be no greater than 7 microns. At least 80% of the fibers should have diameters no greater than 7 microns. Preferably, at least 90% of the fibers should have diameters no greater than 7 microns. A narrow distribution of fiber diameters enhances the potential for achieving the unique balance of properties of this invention. While it is possible to produce fabrics with average fiber diameters greater than 7 microns and obtain high strength, the ultimate repellency of such a fabric would be compromised, and it would then not be feasible to produce low weight fabrics with high repellency.
Applicants have further discovered that when the melt-blown fibrous web is formed in such a manner that autogeneous bonding is very low and the webs have little or no integrity, the fabrics that result upon thermal embossing these webs are much stronger and possess better aesthetics than fabrics made of webs with high initial strength. That is, the weakest unembossed webs, with fiber dimensions as described above, form the strongest embossed fabrics. The higher the level of initial interfiber bonding, the stiffer and more brittle the resulting fabric, leading to poor grab and tear strengths. As autogenous bonding is reduced, the resulting fabric develops not only good strength but becomes softer and more drapable after thermal embossing. Because of the relatively low levels of web integrity, it is useful to determine the strength of the unembossed web by the strip tensile strength method, which uses a 2.54 cm-wide sample and grip facings which are also a minimum 2.54 cm wide (ASTM D1117). In prior art melt blown fabrics the machine direction (MD) strip tensile strength of the autogenously bonded web is generally greater than 30% and frequently up to 70% or more of the strip tensile strength of the bonded fabric. That is, the potential contribution of autogenous bonding to the strength of the embossed fabric is quite high. In the present invention autogenous bonding contributes less than 30%, and preferably less than 10%, of the strip tensile strength of the bonded fabric.
For example, aNylon 6 melt-blown web with a weight of approximately 50 g/m2 made under prior art conditions may possess a strip tensile strength in the machine direction of between 10 to 20 N. In the fabric of this invention, it is necessary to keep the strip tensile strength of the unembossed web below 10 N and preferably below 5 N to achieve the full benefits of the invention. In other words, when long fibers are produced and collected, in such a way that initial interfiber bonding is low, the individual fibers are stronger, and there is greater exploitation of the inherent strength of the fibers themselves.
While it is difficult and tedious to obtain an accurate determination of the strength of individual microdenier fibers, a good reflection of the strength of the fibers can be obtained by using the zero-span strip test method. In the normal strip tensile test, the load cells are set at approximately 7.6 cm apart. At this span length, the application of modest loads in the machine direction to an unembossed web may cause the web to fail from fibers slipping by one another rather than by actually breaking the fibers. This is particularly true if the strength of the individual fibers is much higher than the strength of the autogenous bond. The integrity is then due primarily to the interfiber bonding, i.e., autogenous bonding, and perhaps partially to the length of the fibers and their degree of entanglement. As the span length is decreased, there is a smaller and smaller chance for the fibers to move, and at very short distances, close to zero span, the lengths of the fibers, and interfiber movements, are no longer factors in the values measured. The strength obtained is, therefore, a good reflection of the strength of the individual fibers and the ultimate strength of the fabric.
FIG. 5 illustrates the phenomena described above, and indicates the advantage of achieving high individual fiber strength, and low interfiber bonding of the unembossed web. The plot shows the relationship between breaking strength (strip tensile) and span length for twoNylon 6 melt-blown webs of approximately the same weight, one of which, "A", was produced with characteristics typical of conventional melt-blown processes, and the other, "B", was produced under conditions and with characteristics typical of the present invention. The normal strip tensile test shows "A" to be stronger than "B" by over 300% (11.1 N vs. 3.5 N). At zero span length, the strengths have crossed over, and the tensile strength of "B" is greater by about 93% over "A" (35 N vs. 18.1 N). This indicates that the individual fibers of the webs of the present invention are stronger than the individual fibers of the webs of the prior art. FIG. 6 serves as a further illustration demonstrating that the strength of embossed fabric "B" is greater than the strength of embossed fabric "A". At the normal strip tensile span (7.6 cm), the strength of "B" is almost 200% that of "A" (30.5 N vs. 15.8 N). The processes of preparing "A" and "B" are set forth in Example I. The zero span strip tensile strength to weight ratio in the machine direction (M.D.) of the fabrics of the present invention is greater than 0.4 N·m2 /g and preferably greater than 0.5 N·m2 /g. For fabric applications where very high strengths are required, the zero span strip tensile strengths to weight ratio should be greater than 1.0 N·m2 /g.
In summary, the web of the fabric of the present invention, in contrast to conventional melt-blown webs of the prior art, is characterized by high average fiber length, low interfiber bonding and stronger individual fibers. These characteristics are achieved while maintaining low fiber diameters in a relatively narrow distribution range to provide high resistance to fluid penetration. High aesthetic characteristics are also obtained.
The method of producing the desired web characteristics of the fabric of the invention is based on the control of the key process variables and their interactions to achieve the desired fiber, web, and fabric properties. These process variables include extrusion temperatures, primary air flow and temperature, secondary air flow, and forming length. Since there are many combinations of these factors which can produce different aspects of the present fabric, the influence of these variables on the key desired web properties will now be described in general.
As previously discussed, in order to obtain strong melt-blown fabrics, the individual fibers themselves should possess good strength. In conventional melt-blowing processes, it is generally recommended that the resin in the extruder and die should be maintained at a high enough temperature to degrade the polymer extensively so as to improve polymer flow and avoid the formation of "shot". Shot is defined as a mass of nonfibrous polymer with a diameter greater than 0.3 mm. Typically, the die melt temperature, i.e., the temperature of the polymer melt at the die, is about 100° C. above the melting temperature of the resin. However, excessive degradation of the polymer reduces the potential to form individual fibers with high strength. Applicants have determined that individual fiber strength can be enhanced significantly if the die melt temperature, for instance, can be maintained at levels generally 10° to 35° C. below temperatures recommended for prior art processes. Generally, in the present process the die melt temperature is no greater than about 75° C. above the melting point of the polymer. Obviously, the specific optimum temperature would depend on the polymer being extruded. In general, the level of degradation must be kept as low as possible without forming shot. By proper design of the melt-blowing die, and control of forming air to fiber ratios, shot formation can be avoided or substantially reduced.
The strength of the individual fiber is also dependent on the degree of molecular orientation that is achieved when the extruded fiber is attenuated by the air stream. The rate of attenuation and the rate of cooling of the fibers are, therefore, important. The velocity and temperature of the primary air, and the velocity and temperature of the secondary air must be adjusted to achieve optimum fiber strength, zero span strength, for a given polymer. The high velocity secondary air employed in the present process is instrumental in increasing the time and the distance over which the fibers are attenuated. The cooling effect of the secondary air enhances the probability that the molecular orientation of the fibers is not excessively relaxed on the deceleration of the fibers as they are collected on the screen.
The achievable fiber length also is influenced by the primary and secondary air velocities, the level of degradation of the polymer and, of critical importance, air flow uniformity. In forming the web of the fabric of this invention, it is of extreme importance to maintain a high degree of air and fiber flow uniformity, avoiding large amplitude turbulence, vortices, streaks, and other flow irregularities. Good primary air flow uniformity can be obtained by adhering to standard aerodynamic design guidelines in the design of die air plenums and nozzles. In a conventional melt-blowing process, as the primary air velocity increases and fiber diameters decrease, the fibers are more easily ruptured by high amplitude turbulence. By maintaining high uniformity, breakage of the fibers is minimized and optimum fiber lengths can be achieved. Introduction of high velocity secondary air also serves to control the air/fiber stream, by cooling and maintaining molecular orientation of the fibers so that stronger fibers are produced that are more resistant to possible breakage caused by nonuniform air flow.
In order to deposit the fibers on the forming conveyor as a web with low strip tensile strength, the forming air and forming distance are clearly important. In the present process, the forming distance is generally between 20 and 50 centimeters. First, in order for the web to have minimal interfiber bonding, the fibers must arrive at the forming conveyor in a relatively solid state, free of surface tackiness. To allow the fibers time to solidify, it is possible to set the forming conveyor farther away from the die. However, at excessively long distances, i.e., greater than 50 cm., it is difficult to maintain good uniformity of the air/fiber stream and "roping" may occur. Roping is a phenomenon by which individual fibers get entangled with one another in the air stream to form coarse fiber bundles. Excessive roping diminishes the capacity of the resultant fabric to resist fluid penetration, and also leads to poor aesthetic attributes. A primary air flow of high uniformity enhances the opportunity to achieve good fiber attenuation and relatively long distance forming without roping.
The primary air volume is also an important factor. Sufficient air volume must be used, at a given polymer flow rate and forming length, to maintain good fiber separation in the air/fiber stream, in order to minimize the extent of roping.
The use of the secondary air system also is important in achieving low interfiber bonding without roping. As noted previously, the high velocity secondary air is effective in improving the uniformity of the air/fiber stream. Thus, it enhances the potential to move the forming length beyond prior art distances, without causing undesirable roping. Furthermore, since the secondary air is maintained at ambient temperature, or lower if desired, it can serve also to cool and solidify the fibers in a shorter time, thus obviating the need for detrimentally large forming lengths. For the secondary air system to have an influence on flow uniformity and cooling, and the rate of deceleration of the fibers, its velocity should be high enough that its flow is not completely overwhelmed by the primary air flow. In the present process, a secondary air velocity of 30 m/sec to 200 m/sec or higher is effective in providing the desired air flow characteristics.
Obviously, there are various approaches and combinations of primary and secondary air flows, temperatures, and forming lengths that can be used to achieve low interfiber bonding in the unembossed web. The specific process parameters depend on the polymer being used, the design of the die and its air systems, the production rate, and the desired product properties.
The unembossed web or layers of unembossed webs must be bonded to convert the web or webs to a fabric to be used in applications requiring good integrity. It has been determined to be advantageous to use thermal bonding techniques. Either ultrasonic or mechanical embossing roll systems using heat and pressure may be used. For the present invention, it is preferred to use a mechanical embossing system for point bonding using an engraved roll on one side and a solid smooth roll on the other side of the fabric. In order to avoid "pinholes" in the fabric, it has also been found desirable to set a small gap, of the order of 0.01 mm, between the top and bottom rolls. For the intended use of the fabrics which can be produced by this invention, the total embossed area must be in the range of 5 to 30% of the total fabric surface, and preferably should be in the range of 10-20%. In the examples given to illustrate the invention, the embossed area is 18%. The embossing pattern is 0.76 mm×0.76 mm diamond pattern with 31 diamonds per square centimeter of roll surface. The particular embossing pattern employed is not critical and any pattern bonding between 5 and 30% of the fabric surface may be used.
In order to render the fabric especially effective for use in applications requiring high abrasion resistance, a small amount of chemical binder can be applied by suitable means to the surface of the fabric in small quantities, i.e., less than 10% of fabric weight. An example of such a binder is Primacor 4990 which is an 80/20 copolymer of ethylene and acrylic acid, manufactured by the Dow Chemical Company. For applications requiring repellency, such as for surgical gowns and drapes, the fabric can be treated further with suitable repellent chemicals. Fluorochemicals are normally employed to impart repellency.
The principles of this invention apply to any of the commercially available resins, such as polypropylene, polyethylene, polyamides, polyester or any polymer or polymer blends capable of being melt blown. It has been found particularly advantageous to use polyamides, and particularly Nylon 6 (polycaprolactam), in order to obtain superior aesthetics, low susceptibility to degradation due to cobalt irradiation, excellent balance of properties, and overall ease of processing.
Generally, the fabrics of the present invention have a basis weight of from 14 to 85 grams per square meter. The fabrics have a minimum grab tensile strength to weight ratio greater than 0.8 N per gram per square meter and a minimum Elmendorf tear strength to weight ratio greater than 0.04 N per gram per square meter. For medical fabrics where high strength is required, the fabrics have a basic weight no greater than 60 grams per square meter and have a minimum grab tensile strength of 65 N and a minimum Elmendorf tear strength not less than 6 N.
It is to be understood that the fibers, webs or fabrics produced according to this invention can be combined in various ways, and with other fibers, webs, or fabrics possessing different characteristics to form products with specifically tailored properties.
The examples which follow are intended to clarify further the present invention, and are in no way intended to serve as the limits of the content or scope of this invention.
EXAMPLE 1
Three one-ply melt-blown nylon webs of approximately 50 g/m2 were produced, using for Fabric A, specifications typical of prior art processes. Fabrics B and C were produced using process conditions and fiber and web characteristics typical of the present invention. All three fabrics were then embossed under identical conditions, again with typical settings of the present invention. The strengths of these fabrics were then compared:
______________________________________                                    Process Parameters                                                                      Fabric A   Fabric B Fabric C                                ______________________________________                                    Die melt temperature                                                                    315        280      264                                     (°C.)                                                              Primary air temperature                                                                 334        318      285                                     (°C.)                                                              Air gap/setback (cm)                                                                    .178/.178  .114/.102                                                                          .114/.102                               (neg)                                                                     Polymer flow per cm                                                                     4.8        1.7      1.7                                     of die width (g/min)                                                      Secondary air velocity                                                                   0          30      30                                      (m/sec)                                                                   Forminglength                                                                           22         22      22                                      (collector distance)                                                      (cm)                                                                      Top embossing roll                                                                       99        103      97                                      temperature (°C.)                                                  Bottom embossing roll                                                                    97         98      99                                      temperature (°C.)                                                  Roll separation gap                                                                     0.01       0.01     0.01                                    (mm)                                                                      Fabric Properties                                                         Grab tensile strength                                                     to weight ratio                                                           (N · m.sup.2 /g)                                                 MD            0.67       1.43     1.72                                    CD            0.50       0.96     1.04                                    Elmendorf tear strength                                                   to weight ratio                                                           (N · m.sup.2 /g)                                                 MD            0.03       0.22     0.18                                    CD            0.04       0.31     0.24                                    ______________________________________
Fabrics B and C had superior strength, in both grab tensile and tear strength. In particular, the tear strengths of B and C were dramatically improved over prior art expectations.
EXAMPLE 2
In this example, variations in the method to produce the fabric of this invention were used to illustrate the structural characteristics of the fabric of this invention compared with a fabric based on the same process conditions as specified for Fabric A in Example 1.
All fabrics were produced using single-ply Nylon 6 webs with approximate weight of 50 g/m2.
Fabric A was produced under conditions exemplified in Example 1 (Fabric A). Fabrics D through H were produced under conditions typical of the present invention, all at lower die melt temperatures (264°-280° C.) and high velocity secondary air using various combinations of primary air volume and velocity and secondary air velocity. The strength characteristics of the fabrics were then compared.
______________________________________                                              Fabric                                                          Parameter   A       D      E      F    G    H                             ______________________________________                                    Avg.fiber length                                                                     10      25     25     46   20   46                            (cm)                                                                      Avg. fiber diameter                                                                   2.0     3.7    5.6    4.3  3.5  4.3                           (cm)                                                                      Grab tensile strength:                                                    Ratio (N · m.sup.2 /g)                                           MD          .67     1.33   1.43   1.76 1.45 1.72                          CD          .50     1.07   .96    1.21 .84  1.04                          Tear strength ratio:                                                      Ratio (N · m.sup.2 /g)                                           MD          .03     .20    .22    .15  .08  .18                           CD          .04     .25    .31    .28  .16  .24                           ______________________________________
All of the fabrics produced using conditions described in this application possess not only longer fiber length, but higher strength as well, compared to Fabric A.
EXAMPLE 3
Single-ply Nylon 6 microfiber webs were formed under two different conditions to illustrate the effect of low initial interfiber bonds of the unembossed web on the strength properties of the embossed fabric. Fabric A in this example is the same web and fabric as Fabric A of Example 1, representing prior art melt-blown web structure. Fabric B is the same as Fabric B of Example 1. The two webs were similar in weight of about 50 g/m2. The zero-span strength plots of these webs are shown in FIG. 5.
______________________________________                                    Parameter             Fabric A  Fabric B                                  ______________________________________                                    Strip Tensile Strength (N)                                                                  MD      11.1      3.5                                   (Unembossed)                                                              Zero Span Strip Tensile (N)                                                                 MD      18.1      35                                    (Unembossed)                                                              Strip Tensile (Embossed) (N)                                                                MD      15.8      30.5                                  Grab Tensile Strength (N)                                                                   MD      31.6      73.0                                  (Embossed)        CD      23.5      49.0                                  Tear Strength (N) MD       1.3      11.1                                  (Embossed)        CD       1.7      14.8                                  ______________________________________
The web of Fabric B, with very low initial strip tensile, surprisingly yielded a fabric with excellent strength and aesthetic properties after embossing.
EXAMPLE 4
In order to illustrate the effect of temperature on the strength of melt-blown fabrics, two single-ply nylon webs were produced using identical conditions except for temperature. Thus, the die melt temperature of the web for Fabric "K" was 20° C. lower than for Fabric "J". The webs were also embossed under identical conditions with an embossed area of 18% of the total fabric surface.
______________________________________                                    Parameter         Fabric J Fabric K                                       ______________________________________                                    Polymer rate per cm                                                                         1.7      1.7                                            of width (g/min)                                                          Die melt temperature                                                                        294      274                                            (°C.)                                                              Basis weight (g/m.sup.2)                                                                    46       46                                             Grab tensile strength                                                     (N)                                                                       MD                71       107                                            CD                61       80                                             Intrinsic viscosity                                                                         1.09     1.28                                           (dl/g)                                                                    ______________________________________
As observed, lower temperatures enhance the strength of the fabric as degradation of the polymer is kept at lower levels than standard practice. The intrinsic viscosity values confirm that the polymer in Fabric K was degraded less. The intrinsic viscosity was determined using 90% formic acid at 25° C.
EXAMPLE 5
Melt-blown polypropylene webs were produced, first using typical conditions described in the prior art to obtain webs of conventional structural characteristics. Then, webs were produced using the principles of the present invention. Also, a combination of the two different webs was assembled. All the webs were thermally embossed under identical conditions to produce fabrics. Fabric L was produced under conditions in the range of prior art processes. The web for Fabric M was produced using the principles of the present invention. Fabric N was produced by laminating a 34 g/m2 layer of web M to a 13.5 g/m2 layer of Web L. Fabric O is an example of the properties of a prior art thermally embossed polypropylene melt-blown web as described in U.S. Pat. No. 4,041,203, Example 1. Fabric P was produced under the same conditions as Fabric L, but with high velocity secondary air.
______________________________________                                                Fabric                                                        Process conditions                                                                      L      M       N    O    P                                  ______________________________________                                    Die melt temperature                                                                    279    260     --   --   279                                (°C.)                                                              Primary air tempera-                                                                    315    272     --   --   315                                ture (°C.)                                                         Primary air velocity                                                                    278    153     --   --   278                                (m/sec)                                                                   Polymer flow rate                                                                       1.7    1.7     --   --   1.7                                per cm (g/min)                                                            Forminglength                                                                           15     48     --   --    15                                (collector distance)                                                      (cm)                                                                      Die air gap (mm)                                                                        1.14   1.14    --   --   1.14                               Die setback (mm)                                                                        1.02   1.02    --   --   1.02                               negative                                                                  Secondary air  0      30     --   --    30                                velocity (m/sec)                                                          Fabric Characteristics                                                    Grab tensile strength                                                     to weight ratio                                                           (N · m.sup.2 /g)                                                 MD            0.69   1.13    1.03 0.46 .91                                CD            0.47   0.93    0.88 --   .84                                Elmendorf tear strength                                                   to weight ratio                                                           (N · m.sup.2 /g)                                                 MD            .002   .178    .050 --   .005                               CD            .003   .300    .098 --   .007                               Trapezoidal tear                                                          strength to weight                                                        ratio (N · m.sup.2 /g)                                           (ASTM D1117)                                                              MD            .011   .499    .384 .087 .052                               CD            .025   .876    .601 --   .120                               ______________________________________
Particularly dramatic is the improvement in tear strength demonstracted by Fabrics M and N, far exceeding values obtained with prior art technology.
This example also illustrates that various combinations of different webs can be laminated to produce a variety of fabric properties.
EXAMPLE 6
As described in preceding sections, for gown and drape applications, the requirements of a good fabric are quite demanding. After producing the embossed fabric, it normally has to be further treated to render it repellent in order to resist penetration by the normal fluids encountered in its use. Normally, fluorochemical finishes are employed to impart repellency.
For illustration, a single-ply Nylon 6 web was produced under the following conditions:
______________________________________                                    Die melt temperature  267° C.                                      Primary air temperature                                                                         289° C.                                      Primary air velocity  227 m/sec                                           Polymer flow rate     1.7 g/min/cm                                        Collector distance    27 cm                                               Die air gap           1.14 mm                                             Die set back negative 1.02 mm                                             Secondary air velocity                                                                          30 m/sec                                            ______________________________________
The weight was approximately 49 g/m2. The fabric was sprayed with a fluorochemical solution (Scotchguard) at a level of 5 grams per square meter and dried. The properties of this fabric in key aspects were then compared with those of other fabrics commercially used or available as medical fabrics. In this example,Fabric 1 represents the fabric of this invention,Fabric 2 is produced by hydraulically entangling polyester staple fibers with pulp fibers. It is commercially available under the trandemark "Sontara" and manufactured by the E. I. du Pont de Nemours & Company of Wilmington, Del. It is widely used as a medical fabric.Fabric 3 is produced by thermally emboss-laminating continuous fiber (spunbonded) polypropylene web layers on both sides of a melt-blown polypropylene layer. The fabric is commercially used as a medical fabric under the trademark "Spunguard", manufactured by Kimberly-Clark Corporation of Neenah, Wis.Fabric 4 is an example of a wood pulp/polyester blended nonwoven fabric available from the C. H. Dexter Corporation as Assure III.Fabric 5 is a three-component laminate comprising two plies of tissue around a layer of spunbonded nylon core. The fabric has been used as a medical fabric and commercially available as "Boundary--Fabric III".Fabric 6 is another example of a laminate structure with outside layers of tissue on each side of a scrim core. The fabric is trademarked "Regard", manufactured by Kimberly-Clark. It has been used commonly as a medical fabric.Fabric 7 is a low denier thermally embossed spunbonded polyethylene fabric manufactured by E. I. du Pont under the tradename "Tyvek". It is available and has been used as a medical fabric.
______________________________________                                    Fabric                                                                          W      HH     GTS*    TS*  FAP    TH   CDC                          ______________________________________                                    1     52     49     81       10  18     .32  44                           2     75     25     69      >16  24     .34  45                           3     49     42     50        2  11     .32  70                           4     69     26     75      >16  24     .25  92                           5     75     24     60        6  12     .29  65                           6     75     25     53        6   6     .34  78                           7     48     75     66      >16   1     .20  80                           ______________________________________                                     *Weakest direction                                                        NOTE:                                                                     W: Basis weight (g/m.sup.2)                                               HH: Hydrostatic head (cm, H.sub.2 O)                                      GTS: Grab tensile strength (N)                                            TS: Elmendorf tear strength (N)                                           FAP: Frazier air porosity (m.sup.3 /min - m.sup.2)                        TH: Thickness (mm)                                                        CDC: Cusick drape coefficient (%)
The ideal medical fabric would, of course, have high hydrostatic head, high strength, high breathability, low weight (especially for gowns), with high bulk so as not to be "flimsy" in use as drapes, and low Cusick drape coefficient. Because of inherent limitations, and as illustrated in the above table, most fabrics achieve one desirable characteristic only at considerable expense of other important characteristics. In order to facilitate comparison of the properties shown in the table, and to evaluate the balance of properties achieved by each fabric, the absolute value of each property can be normalized such that for each fabric characteristic, the fabric with the highest value can be assigned a value of 1. All other fabrics will then have properties reflected as fractions of the highest value. A normalized chart is shown in the following table.
______________________________________                                    Fabric                                                                          W        HH     GTS    TS*  FAP   TH   CDC                          ______________________________________                                    1     .69      .65    1.00   .63  .75   .94  .48                          2     1.00     .33    .85    1.00 1.00  1.00 .49                          3     .65      .56    .62    .13  .46   .94  .76                          4     .92      .35    .93    1.00 1.00  .74  1.00                         5     1.00     .32    .74    .38  .50   .85  .71                          6     1.00     .33    .65    .38  .25   1.00 .85                          7     .64      1.00   .82    1.00 .04   .59  .87                          ______________________________________                                     *The maximum tear strength is assumed to be 16 N. Fabrics with tear value at this level or above, meet all criteria necessary for any medical       application.
A performance index of each fabric can now be computed from the ratio: ##EQU1##
The performance indices are listed below:
______________________________________                                                 Performance                                                         Fabric                                                                          Index                                                        ______________________________________                                           1     .88                                                                 2     .57                                                                 3     .04                                                                 4     .26                                                                 5     .05                                                                 6     .02                                                                 7     .04                                                          ______________________________________
These indices demonstrate the unique and superior balance of properties achieved by the present invention, compared to prior art fabrics.

Claims (11)

We claim:
1. A nonreinforced melt blown microfiber embossed fabric having a minimum grab tensile strength to weight ratio greater than 0.8 N per gram per square meter, and having a minimum Elmendorf tear strength to weight ratio greater than 0.04 N per gram per square meter.
2. The fabric of claim 1 where the basis weight is in the range of 14 g/m2 to 85 g/m2.
3. The fabric of claim 1 in which the fabric is thermally embossed at intermittent discrete bond regions which occupy between 5 and 30% of the surface of the fabric.
4. The fabric of claim 1 in which the average fiber length is greater than 10 cm.
5. The fabric of claim 1 where the basis weight is no greater than 60 g/m2 and the minimum grab tensile strength is not less than 65 N and the minimum Elmendorf tear strength is not less than 6 N.
6. The fabric of claim 1 in which the average fiber length of the fibers is greater than 20 cm.
7. A nonreinforced melt blown fabric comprising a microfiber web in which at least 80% of the fibers have a diameter of 7 microns or less, and in which the autogenous bonding of the fibers contribute no more than 30% of the strip tensile strength of the fabric, said fabric being thermally embossed at intermittent discrete bond regions which occupy between 5 and 30% of the surface of the web and having a minimum grab tensile strength to weight ratio greater than 0.8 N per gram per square meter and an Elmendorf tear strength to weight ratio greater than 0.04 N per gram per square meter.
8. The fabric of claim 7 in which the average fiber length of the fibers in the web is greater than 10 centimeters.
9. The fabric of claim 7 in which the average fiber length of the fibers in the web is at least 20 centimeters.
10. The fabric of claim 7 in which at least 90% of the fibers have a diameter of 7 microns or less.
11. The fabric of claim 7 in which the basis weight of the fabric is between 14 and 85 grams per square meter.
US06/763,5081985-08-081985-08-08Nonwoven medical fabricExpired - LifetimeUS4622259A (en)

Priority Applications (11)

Application NumberPriority DateFiling DateTitle
US06/763,508US4622259A (en)1985-08-081985-08-08Nonwoven medical fabric
US06/884,563US4908163A (en)1985-08-081986-07-11Nonwoven medical fabric
NZ216982ANZ216982A (en)1985-08-081986-07-25Non-reinforced melt blown embossed medical fabric: 80% of fibres have a diameter of 7 microns or less
CA000515440ACA1318993C (en)1985-08-081986-08-06Nonwoven medical fabric
AU60941/86AAU592811B2 (en)1985-08-081986-08-06Nonwoven medical fabric
BR8603783ABR8603783A (en)1985-08-081986-08-07 CLOTH AND PROCESS FOR YOUR PRODUCTION
DE8686111123TDE3687053T2 (en)1985-08-081986-08-07 FLEECE FOR MEDICAL PURPOSES.
JP61184343AJPS6245763A (en)1985-08-081986-08-07Medical nonwoven fabric
ZA865951AZA865951B (en)1985-08-081986-08-07Nonwoven medical fabric
ES8600929AES2001071A6 (en)1985-08-081986-08-07Nonwoven medical fabric.
EP86111123AEP0212540B1 (en)1985-08-081986-08-07Nonwoven medical fabric

Applications Claiming Priority (1)

Application NumberPriority DateFiling DateTitle
US06/763,508US4622259A (en)1985-08-081985-08-08Nonwoven medical fabric

Related Child Applications (1)

Application NumberTitlePriority DateFiling Date
US06/884,563DivisionUS4908163A (en)1985-08-081986-07-11Nonwoven medical fabric

Publications (1)

Publication NumberPublication Date
US4622259Atrue US4622259A (en)1986-11-11

Family

ID=25068022

Family Applications (2)

Application NumberTitlePriority DateFiling Date
US06/763,508Expired - LifetimeUS4622259A (en)1985-08-081985-08-08Nonwoven medical fabric
US06/884,563Expired - LifetimeUS4908163A (en)1985-08-081986-07-11Nonwoven medical fabric

Family Applications After (1)

Application NumberTitlePriority DateFiling Date
US06/884,563Expired - LifetimeUS4908163A (en)1985-08-081986-07-11Nonwoven medical fabric

Country Status (10)

CountryLink
US (2)US4622259A (en)
EP (1)EP0212540B1 (en)
JP (1)JPS6245763A (en)
AU (1)AU592811B2 (en)
BR (1)BR8603783A (en)
CA (1)CA1318993C (en)
DE (1)DE3687053T2 (en)
ES (1)ES2001071A6 (en)
NZ (1)NZ216982A (en)
ZA (1)ZA865951B (en)

Cited By (108)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US4714647A (en)*1986-05-021987-12-22Kimberly-Clark CorporationMelt-blown material with depth fiber size gradient
US4774125A (en)*1985-10-021988-09-27Surgikos, Inc.Nonwoven fabric with improved abrasion resistance
US4818600A (en)*1987-12-091989-04-04Kimberly-Clark CorporationLatex coated breathable barrier
US4988560A (en)*1987-12-211991-01-29Minnesota Mining And Manufacturing CompanyOriented melt-blown fibers, processes for making such fibers, and webs made from such fibers
US4999235A (en)*1987-07-241991-03-12Ethicon, Inc.Conformable, stretchable surgical wound closure tape
US5075068A (en)*1990-10-111991-12-24Exxon Chemical Patents Inc.Method and apparatus for treating meltblown filaments
US5141699A (en)*1987-12-211992-08-25Minnesota Mining And Manufacturing CompanyProcess for making oriented melt-blown microfibers
US5196207A (en)*1992-01-271993-03-23Kimberly-Clark CorporationMeltblown die head
US5231463A (en)*1991-11-201993-07-27The Board Of Regents Of The University Of OklahomaMethod for on-line fiber flow measurement
US5405559A (en)*1993-12-081995-04-11The Board Of Regents Of The University Of OklahomaPolymer processing using pulsating fluidic flow
US5409765A (en)*1993-08-041995-04-25Fiberweb North America, Inc.Nonwoven webs made from ionomers
US5482765A (en)*1994-04-051996-01-09Kimberly-Clark CorporationNonwoven fabric laminate with enhanced barrier properties
US5614306A (en)*1991-12-311997-03-25Kimberly-Clark CorporationConductive fabric and method of producing same
US5667749A (en)*1995-08-021997-09-16Kimberly-Clark Worldwide, Inc.Method for the production of fibers and materials having enhanced characteristics
US5688157A (en)*1994-04-051997-11-18Kimberly-Clark Worldwide, Inc.Nonwoven fabric laminate with enhanced barrier properties
US5698481A (en)*1994-10-121997-12-16Kimberly-Clark Worldwide, Inc.Sterilization wrap material
US5705251A (en)*1995-06-271998-01-06Kimberly-Clark Worldwide, Inc.Garment with liquid intrusion protection
US5711970A (en)*1995-08-021998-01-27Kimberly-Clark Worldwide, Inc.Apparatus for the production of fibers and materials having enhanced characteristics
US5807366A (en)1994-12-081998-09-15Milani; JohnAbsorbent article having a particle size gradient
US5810954A (en)*1996-02-201998-09-22Kimberly-Clark Worldwide, Inc.Method of forming a fine fiber barrier fabric with improved drape and strength of making same
US5811178A (en)*1995-08-021998-09-22Kimberly-Clark Worldwide, Inc.High bulk nonwoven sorbent with fiber density gradient
US5814570A (en)1994-06-271998-09-29Kimberly-Clark Worldwide, Inc.Nonwoven barrier and method of making the same
US5821178A (en)1994-12-301998-10-13Kimberly-Clark Worldwide, Inc.Nonwoven laminate barrier material
US5830810A (en)*1995-07-191998-11-03Kimberly-Clark Worldwide, Inc.Nonwoven barrier and method of making the same
US5834384A (en)1995-11-281998-11-10Kimberly-Clark Worldwide, Inc.Nonwoven webs with one or more surface treatments
US5877099A (en)*1995-05-251999-03-02Kimberly Clark CoFilter matrix
US5885909A (en)*1996-06-071999-03-23E. I. Du Pont De Nemours And CompanyLow or sub-denier nonwoven fibrous structures
WO1999023983A1 (en)1997-11-101999-05-20The Procter & Gamble CompanyDisposable absorbent article having improved soft barrier cuff
US5913329A (en)*1995-12-151999-06-22Kimberly-Clark Worldwide, Inc.High temperature, high speed rotary valve
US5993943A (en)*1987-12-211999-11-303M Innovative Properties CompanyOriented melt-blown fibers, processes for making such fibers and webs made from such fibers
US5998308A (en)1994-02-221999-12-07Kimberly-Clark Worldwide, Inc.Nonwoven barrier and method of making the same
US6365088B1 (en)1998-06-262002-04-02Kimberly-Clark Worldwide, Inc.Electret treatment of high loft and low density nonwoven webs
US6420627B1 (en)1997-11-102002-07-16The Procter & Gamble CompanyDisposable absorbent article having improved soft barrier cuff
US6441267B1 (en)1999-04-052002-08-27Fiber Innovation TechnologyHeat bondable biodegradable fiber
US6444312B1 (en)1999-12-082002-09-03Fiber Innovation Technology, Inc.Splittable multicomponent fibers containing a polyacrylonitrile polymer component
EP1194626A4 (en)*1999-06-162002-12-04First Quality Nonwovens IncImproved method of making media of controlled porosity and product thereof
US20030003834A1 (en)*2000-11-202003-01-023M Innovative Properties CompanyMethod for forming spread nonwoven webs
US6509092B1 (en)1999-04-052003-01-21Fiber Innovation TechnologyHeat bondable biodegradable fibers with enhanced adhesion
US20030017776A1 (en)*1999-12-222003-01-23Kazuyuki OhnishiDisposable garment comprising meltblown nonwoven backsheet
US6537932B1 (en)1997-10-312003-03-25Kimberly-Clark Worldwide, Inc.Sterilization wrap, applications therefor, and method of sterilizing
US6573205B1 (en)1999-01-302003-06-03Kimberly-Clark Worldwide, Inc.Stable electret polymeric articles
US6583075B1 (en)1999-12-082003-06-24Fiber Innovation Technology, Inc.Dissociable multicomponent fibers containing a polyacrylonitrile polymer component
US20030119410A1 (en)*1999-06-162003-06-26Hassan BodaghiMethod of making media of controlled porosity and product thereof
US20030147983A1 (en)*2000-11-202003-08-073M Innovative PropertiesFiber-forming apparatus
US6607624B2 (en)2000-11-202003-08-193M Innovative Properties CompanyFiber-forming process
US6613268B2 (en)2000-12-212003-09-02Kimberly-Clark Worldwide, Inc.Method of increasing the meltblown jet thermal core length via hot air entrainment
US20030216099A1 (en)*2002-05-202003-11-203M Innovative Properties CompanyNonwoven amorphous Fibrous webs and methods for making them
US20030216096A1 (en)*2002-05-202003-11-203M Innovative Properties CompanyBondable, oriented, nonwoven fibrous webs and methods for making them
US6667254B1 (en)2000-11-202003-12-233M Innovative Properties CompanyFibrous nonwoven webs
US20040097158A1 (en)*1996-06-072004-05-20Rudisill Edgar N.Nonwoven fibrous sheet structures
US6759356B1 (en)1998-06-302004-07-06Kimberly-Clark Worldwide, Inc.Fibrous electret polymeric articles
US6767498B1 (en)1998-10-062004-07-27Hills, Inc.Process of making microfilaments
US6780357B2 (en)1999-09-152004-08-24Fiber Innovation Technology, Inc.Splittable multicomponent polyester fibers
US6838402B2 (en)1999-09-212005-01-04Fiber Innovation Technology, Inc.Splittable multicomponent elastomeric fibers
US6858297B1 (en)2004-04-052005-02-223M Innovative Properties CompanyAligned fiber web
US6858551B1 (en)1996-05-242005-02-22Kimberly-Clark Worldwide, Inc.Ferroelectric fibers and applications therefor
US20050217226A1 (en)*2004-04-052005-10-063M Innovative Properties CompanyPleated aligned web filter
EP1637632A1 (en)*2004-09-172006-03-22Reifenhäuser GmbH & Co. MaschinenfabrikDevice for producing filaments from thermoplastic material
US20060261525A1 (en)*2005-05-232006-11-23Breister James CMethods and apparatus for meltblowing of polymeric material utilizing fluid flow from an auxiliary manifold
US20060265169A1 (en)*2005-05-232006-11-23Breister James CManifolds for delivering fluids having a desired mass flow profile and methods for designing the same
US20060283259A1 (en)*2005-06-212006-12-21Unger Marketing International, LlcMethod of grading microfiber cleaning cloths
US20080026688A1 (en)*2006-07-252008-01-31Paul MusickMethod and system for maintaining computer and data rooms
US20080160861A1 (en)*2006-12-282008-07-03Berrigan Michael RDimensionally stable bonded nonwoven fibrous webs
US20110037194A1 (en)*2009-08-142011-02-17Michael David JamesDie assembly and method of using same
US7939010B2 (en)2003-04-082011-05-10The Procter & Gamble CompanyMethod for forming fibers
US20110147976A1 (en)*2007-11-092011-06-23Hollingsworth & Vose CompanyMeltblown filter medium
WO2011111028A1 (en)2010-03-112011-09-15Arjowiggins Palalda SasBiodegradable medical material
WO2013082381A1 (en)2011-12-022013-06-06W. L. Gore & Associates, Inc.Heat-stabilized composite filter media and method of making the filter media
US8679218B2 (en)2010-04-272014-03-25Hollingsworth & Vose CompanyFilter media with a multi-layer structure
US20150027380A1 (en)*2011-12-212015-01-29Unicharm CorporationPet sheet
US8950587B2 (en)2009-04-032015-02-10Hollingsworth & Vose CompanyFilter media suitable for hydraulic applications
US8986432B2 (en)2007-11-092015-03-24Hollingsworth & Vose CompanyMeltblown filter medium, related applications and uses
US20150150212A1 (en)*2012-07-062015-06-04Uni-Charm CorporationSheet for pets
EP2918709A1 (en)2014-03-132015-09-16Fiber Innovation Technology, Inc.Multicomponent Aliphatic Polyester Fibers
WO2015164447A2 (en)2014-04-222015-10-29Fiber Innovation Technology, Inc.Fibers comprising an aliphatic polyester blend, and yarns, tows, and fabrics formed therefrom
US9694306B2 (en)2013-05-242017-07-04Hollingsworth & Vose CompanyFilter media including polymer compositions and blends
CN108589044A (en)*2018-06-262018-09-28桐乡守敬应用技术研究院有限公司A kind of melt-blow nonwoven processing unit (plant)
CN108691094A (en)*2018-06-262018-10-23桐乡守敬应用技术研究院有限公司A kind of melt-blow nonwoven processing unit (plant) that can uniformly mix staple fiber
US10155186B2 (en)2010-12-172018-12-18Hollingsworth & Vose CompanyFine fiber filter media and processes
US10343095B2 (en)2014-12-192019-07-09Hollingsworth & Vose CompanyFilter media comprising a pre-filter layer
WO2020020933A1 (en)*2018-07-272020-01-30Oerlikon Textile Gmbh & Co. KgMelt-spinning device for extruding very fine polymer particles
US10653986B2 (en)2010-12-172020-05-19Hollingsworth & Vose CompanyFine fiber filter media and processes
CN112176435A (en)*2020-10-142021-01-05安徽伯辉智能装备有限公司Melt cooling device for melt-blown non-woven fabric production
US10959456B2 (en)2014-09-122021-03-30R.J. Reynolds Tobacco CompanyNonwoven pouch comprising heat sealable binder fiber
US11019840B2 (en)2014-07-022021-06-01R.J. Reynolds Tobacco CompanyOral pouch products
WO2021116852A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedOral product with dissolvable component
WO2021116919A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedFleece for oral product with releasable component
WO2021116884A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedLayered fleece for pouched product
WO2021116881A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedOral product in a pourous pouch comprising a fleece material
WO2021116853A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedFibrous fleece material
WO2021116917A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedOral composition with nanocrystalline cellulose
WO2021116894A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedPouched products with heat sealable binder
WO2022162558A1 (en)2021-01-282022-08-04Nicoventures Trading LimitedMethod for sealing pouches
US11447893B2 (en)2017-11-222022-09-20Extrusion Group, LLCMeltblown die tip assembly and method
WO2022224196A1 (en)2021-04-222022-10-27Nicoventures Trading LimitedOrally dissolving films
WO2022229926A1 (en)2021-04-302022-11-03Nicoventures Trading LimitedMulti-compartment oral pouched product
WO2023084499A1 (en)2021-11-152023-05-19Nicoventures Trading LimitedProducts with enhanced sensory characteristics
WO2023084498A1 (en)2021-11-152023-05-19Nicoventures Trading LimitedOral products with nicotine-polymer complex
WO2023194959A1 (en)2022-04-062023-10-12Nicoventures Trading LimitedPouched products with heat sealable binder
US11787152B2 (en)2018-12-132023-10-17North Carolina State UniversityMethod of preparing a composite sheet
US11832640B2 (en)2014-12-052023-12-05R.J. Reynolds Tobacco CompanyCapsule-containing pouched product for oral use
WO2024079722A1 (en)2022-10-142024-04-18Nicoventures Trading LimitedCapsule-containing pouched products
WO2024089588A1 (en)2022-10-242024-05-02Nicoventures Trading LimitedShaped pouched products
WO2024095164A1 (en)2022-11-012024-05-10Nicoventures Trading LimitedProducts with spherical filler
WO2024180481A1 (en)2023-02-282024-09-06Nicoventures Trading LimitedCaffeine-containing oral product
US12138342B2 (en)2019-12-092024-11-12Nicoventures Trading LimitedFleece for oral product with releasable component
US12178905B2 (en)2019-12-092024-12-31Nicoventures Trading LimitedFleece for pouched product with controlled basis weight
EP4599698A1 (en)2024-02-072025-08-13Nicoventures Trading LimitedProducts comprising sensory agents

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
JPH0222317U (en)*1988-07-291990-02-14
US5145631A (en)*1990-01-041992-09-08The Dow Chemical CompanyMelt blowing process for producing microfibers of syndiotactic vinyl aromatic polymers
US6406674B1 (en)1993-06-302002-06-18Kimberly-Clark Worldwide, Inc.Single step sterilization wrap system
CA2111071E (en)*1993-06-302011-08-23Sonya Nicholson BourneSingle step sterilization wrap system
US5616408A (en)*1995-12-221997-04-01Fiberweb North America, Inc.Meltblown polyethylene fabrics and processes of making same
US6001303A (en)*1997-12-191999-12-14Kimberly-Clark Worldwide, Inc.Process of making fibers
US6264872B1 (en)*1997-12-302001-07-24Kimberly-Clark Worldwide, Inc.Method of forming thin, embossed, textured barrier films
JP2000051358A (en)*1998-08-172000-02-22Teijin LtdAuxiliary tool of intermittent positive pressure ventilation therapy treating tool
US6247911B1 (en)*1999-05-202001-06-19The University Of Tennessee Research CorporationMelt blowing die
US6413344B2 (en)1999-06-162002-07-02First Quality Nonwovens, Inc.Method of making media of controlled porosity
US6517648B1 (en)*2001-11-022003-02-11Appleton Papers Inc.Process for preparing a non-woven fibrous web
US7014441B2 (en)*2002-11-012006-03-21Kimberly-Clark Worldwide, Inc.Fiber draw unit nozzles for use in polymer fiber production
US7922983B2 (en)2005-07-282011-04-12Kimberly-Clark Worldwide, Inc.Sterilization wrap with additional strength sheet
EP1993461A1 (en)*2006-02-212008-11-26Ahlstrom CorporationNonwoven medical fabric
KR101781707B1 (en)2010-12-062017-09-25미쓰이 가가쿠 가부시키가이샤Melt-blown nonwoven fabric, and production method and device for same
KR101326506B1 (en)*2012-04-302013-11-08현대자동차주식회사Manufacturing method of melt-blown fabric web having random and bulky caricteristics and manufacuring apparatus thereof
JP5877913B1 (en)*2014-08-202016-03-08旭化成建材株式会社 Phenol resin foam laminate and method for producing the same

Citations (3)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US4307143A (en)*1977-10-171981-12-22Kimberly-Clark CorporationMicrofiber oil and water pipe
US4469734A (en)*1981-11-241984-09-04Kimberly-Clark LimitedMicrofibre web products
US4493868A (en)*1982-12-141985-01-15Kimberly-Clark CorporationHigh bulk bonding pattern and method

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US2988469A (en)*1959-12-221961-06-13American Viscose CorpMethod for the production of reticulated webs
US4100324A (en)*1974-03-261978-07-11Kimberly-Clark CorporationNonwoven fabric and method of producing same
US3959421A (en)*1974-04-171976-05-25Kimberly-Clark CorporationMethod for rapid quenching of melt blown fibers
US4526733A (en)*1982-11-171985-07-02Kimberly-Clark CorporationMeltblown die and method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US4307143A (en)*1977-10-171981-12-22Kimberly-Clark CorporationMicrofiber oil and water pipe
US4469734A (en)*1981-11-241984-09-04Kimberly-Clark LimitedMicrofibre web products
US4493868A (en)*1982-12-141985-01-15Kimberly-Clark CorporationHigh bulk bonding pattern and method

Cited By (168)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US4774125A (en)*1985-10-021988-09-27Surgikos, Inc.Nonwoven fabric with improved abrasion resistance
US4714647A (en)*1986-05-021987-12-22Kimberly-Clark CorporationMelt-blown material with depth fiber size gradient
US4999235A (en)*1987-07-241991-03-12Ethicon, Inc.Conformable, stretchable surgical wound closure tape
US4818600A (en)*1987-12-091989-04-04Kimberly-Clark CorporationLatex coated breathable barrier
US5141699A (en)*1987-12-211992-08-25Minnesota Mining And Manufacturing CompanyProcess for making oriented melt-blown microfibers
US4988560A (en)*1987-12-211991-01-29Minnesota Mining And Manufacturing CompanyOriented melt-blown fibers, processes for making such fibers, and webs made from such fibers
US5993943A (en)*1987-12-211999-11-303M Innovative Properties CompanyOriented melt-blown fibers, processes for making such fibers and webs made from such fibers
WO1992007122A1 (en)*1990-10-111992-04-30Exxon Chemical Patents Inc.Method and apparatus for treating meltblown filaments
JP3037420B2 (en)1990-10-112000-04-24ザ・ユニバーシティ・オブ・テネシー・リサーチ・コーポレーション Method and apparatus for treating meltblown filaments
US5075068A (en)*1990-10-111991-12-24Exxon Chemical Patents Inc.Method and apparatus for treating meltblown filaments
US5231463A (en)*1991-11-201993-07-27The Board Of Regents Of The University Of OklahomaMethod for on-line fiber flow measurement
US5614306A (en)*1991-12-311997-03-25Kimberly-Clark CorporationConductive fabric and method of producing same
US5196207A (en)*1992-01-271993-03-23Kimberly-Clark CorporationMeltblown die head
US5409765A (en)*1993-08-041995-04-25Fiberweb North America, Inc.Nonwoven webs made from ionomers
US5433993A (en)*1993-12-081995-07-18The Board Of Regents Of The University Of OklahomaPolymer processing using pulsating fluidic flow
US5523033A (en)*1993-12-081996-06-04The Board Of Regents Of The University Of OklahomaPolymer processing using pulsating fluidic flow
US5405559A (en)*1993-12-081995-04-11The Board Of Regents Of The University Of OklahomaPolymer processing using pulsating fluidic flow
US5998308A (en)1994-02-221999-12-07Kimberly-Clark Worldwide, Inc.Nonwoven barrier and method of making the same
US5482765A (en)*1994-04-051996-01-09Kimberly-Clark CorporationNonwoven fabric laminate with enhanced barrier properties
US5688157A (en)*1994-04-051997-11-18Kimberly-Clark Worldwide, Inc.Nonwoven fabric laminate with enhanced barrier properties
US5814570A (en)1994-06-271998-09-29Kimberly-Clark Worldwide, Inc.Nonwoven barrier and method of making the same
US5698481A (en)*1994-10-121997-12-16Kimberly-Clark Worldwide, Inc.Sterilization wrap material
US5698294A (en)*1994-10-121997-12-16Kimberly-Clark Worldwide, Inc.Sterilization wrap material
US5807366A (en)1994-12-081998-09-15Milani; JohnAbsorbent article having a particle size gradient
US5916204A (en)1994-12-081999-06-29Kimberly-Clark Worldwide, Inc.Method of forming a particle size gradient in an absorbent article
US5821178A (en)1994-12-301998-10-13Kimberly-Clark Worldwide, Inc.Nonwoven laminate barrier material
US5877099A (en)*1995-05-251999-03-02Kimberly Clark CoFilter matrix
US5705251A (en)*1995-06-271998-01-06Kimberly-Clark Worldwide, Inc.Garment with liquid intrusion protection
US5830810A (en)*1995-07-191998-11-03Kimberly-Clark Worldwide, Inc.Nonwoven barrier and method of making the same
US5667749A (en)*1995-08-021997-09-16Kimberly-Clark Worldwide, Inc.Method for the production of fibers and materials having enhanced characteristics
US5807795A (en)*1995-08-021998-09-15Kimberly-Clark Worldwide, Inc.Method for producing fibers and materials having enhanced characteristics
US5811178A (en)*1995-08-021998-09-22Kimberly-Clark Worldwide, Inc.High bulk nonwoven sorbent with fiber density gradient
US5711970A (en)*1995-08-021998-01-27Kimberly-Clark Worldwide, Inc.Apparatus for the production of fibers and materials having enhanced characteristics
US5834384A (en)1995-11-281998-11-10Kimberly-Clark Worldwide, Inc.Nonwoven webs with one or more surface treatments
US5913329A (en)*1995-12-151999-06-22Kimberly-Clark Worldwide, Inc.High temperature, high speed rotary valve
US5810954A (en)*1996-02-201998-09-22Kimberly-Clark Worldwide, Inc.Method of forming a fine fiber barrier fabric with improved drape and strength of making same
US6858551B1 (en)1996-05-242005-02-22Kimberly-Clark Worldwide, Inc.Ferroelectric fibers and applications therefor
US20040152387A1 (en)*1996-06-072004-08-05Rudisill Edgar N.Nonwoven fibrous sheet structures
US20040097158A1 (en)*1996-06-072004-05-20Rudisill Edgar N.Nonwoven fibrous sheet structures
US5885909A (en)*1996-06-071999-03-23E. I. Du Pont De Nemours And CompanyLow or sub-denier nonwoven fibrous structures
US6537932B1 (en)1997-10-312003-03-25Kimberly-Clark Worldwide, Inc.Sterilization wrap, applications therefor, and method of sterilizing
WO1999023983A1 (en)1997-11-101999-05-20The Procter & Gamble CompanyDisposable absorbent article having improved soft barrier cuff
US6420627B1 (en)1997-11-102002-07-16The Procter & Gamble CompanyDisposable absorbent article having improved soft barrier cuff
US6365088B1 (en)1998-06-262002-04-02Kimberly-Clark Worldwide, Inc.Electret treatment of high loft and low density nonwoven webs
US6759356B1 (en)1998-06-302004-07-06Kimberly-Clark Worldwide, Inc.Fibrous electret polymeric articles
US6767498B1 (en)1998-10-062004-07-27Hills, Inc.Process of making microfilaments
US6573205B1 (en)1999-01-302003-06-03Kimberly-Clark Worldwide, Inc.Stable electret polymeric articles
US6893990B2 (en)1999-01-302005-05-17Kimberly Clark Worldwide, Inc.Stable electret polymeric articles
US20030207642A1 (en)*1999-01-302003-11-06Myers David LewisStable electret polymeric articles
US6509092B1 (en)1999-04-052003-01-21Fiber Innovation TechnologyHeat bondable biodegradable fibers with enhanced adhesion
US6441267B1 (en)1999-04-052002-08-27Fiber Innovation TechnologyHeat bondable biodegradable fiber
US20030119410A1 (en)*1999-06-162003-06-26Hassan BodaghiMethod of making media of controlled porosity and product thereof
EP1194626A4 (en)*1999-06-162002-12-04First Quality Nonwovens IncImproved method of making media of controlled porosity and product thereof
US20040265583A1 (en)*1999-09-152004-12-30Fiber Innovation Technology, Inc.Splittable multicomponent polyester fibers
US6780357B2 (en)1999-09-152004-08-24Fiber Innovation Technology, Inc.Splittable multicomponent polyester fibers
US6838402B2 (en)1999-09-212005-01-04Fiber Innovation Technology, Inc.Splittable multicomponent elastomeric fibers
US6444312B1 (en)1999-12-082002-09-03Fiber Innovation Technology, Inc.Splittable multicomponent fibers containing a polyacrylonitrile polymer component
US6583075B1 (en)1999-12-082003-06-24Fiber Innovation Technology, Inc.Dissociable multicomponent fibers containing a polyacrylonitrile polymer component
US7967805B2 (en)1999-12-222011-06-28The Procter & Gamble CompanyDisposable garment comprising meltblown nonwoven backsheet
US7195621B2 (en)1999-12-222007-03-27The Procter & Gamble CompanyDisposable garment comprising meltblown nonwoven backsheet
US7404811B2 (en)1999-12-222008-07-29The Procter & Gamble CompanyDisposable garment comprising meltblown nonwoven backsheet
US20070203469A1 (en)*1999-12-222007-08-30Kazuyuki OhnishiDisposable garment comprising meltblown nonwoven backsheet
US20030017776A1 (en)*1999-12-222003-01-23Kazuyuki OhnishiDisposable garment comprising meltblown nonwoven backsheet
US20080300567A1 (en)*1999-12-222008-12-04Kazuyuki OhnishiDisposable Garment Comprising Meltblown Nonwoven Backsheet
US6824372B2 (en)2000-11-202004-11-303M Innovative Properties CompanyFiber-forming apparatus
US20030147983A1 (en)*2000-11-202003-08-073M Innovative PropertiesFiber-forming apparatus
US6607624B2 (en)2000-11-202003-08-193M Innovative Properties CompanyFiber-forming process
US7470389B2 (en)2000-11-202008-12-303M Innovative Properties CompanyMethod for forming spread nonwoven webs
US20030162457A1 (en)*2000-11-202003-08-283M Innovative PropertiesFiber products
US20030003834A1 (en)*2000-11-202003-01-023M Innovative Properties CompanyMethod for forming spread nonwoven webs
US20050140067A1 (en)*2000-11-202005-06-303M Innovative Properties CompanyMethod for forming spread nonwoven webs
US20040113309A1 (en)*2000-11-202004-06-173M Innovative Properties CompanyFibrous nonwoven webs
US6667254B1 (en)2000-11-202003-12-233M Innovative Properties CompanyFibrous nonwoven webs
US6613268B2 (en)2000-12-212003-09-02Kimberly-Clark Worldwide, Inc.Method of increasing the meltblown jet thermal core length via hot air entrainment
US20050161156A1 (en)*2002-05-202005-07-283M Innovative Properties CompanyBondable, oriented, nonwoven fibrous webs and methods for making them
US6916752B2 (en)2002-05-202005-07-123M Innovative Properties CompanyBondable, oriented, nonwoven fibrous webs and methods for making them
US20030216099A1 (en)*2002-05-202003-11-203M Innovative Properties CompanyNonwoven amorphous Fibrous webs and methods for making them
US7591058B2 (en)2002-05-202009-09-223M Innovative Properties CompanyNonwoven amorphous fibrous webs and methods for making them
US7695660B2 (en)2002-05-202010-04-133M Innovative Properties CompanyBondable, oriented, nonwoven fibrous webs and methods for making them
US7279440B2 (en)2002-05-202007-10-093M Innovative Properties CompanyNonwoven amorphous fibrous webs and methods for making them
US20030216096A1 (en)*2002-05-202003-11-203M Innovative Properties CompanyBondable, oriented, nonwoven fibrous webs and methods for making them
US7939010B2 (en)2003-04-082011-05-10The Procter & Gamble CompanyMethod for forming fibers
US20050217226A1 (en)*2004-04-052005-10-063M Innovative Properties CompanyPleated aligned web filter
US7622063B2 (en)2004-04-052009-11-243M Innovative Properties CompanyPleated aligned web filter
US20100050582A1 (en)*2004-04-052010-03-043M Innovative Properties CompanyPleated aligned web filter
US8142538B2 (en)2004-04-052012-03-273M Innovative Properties CompanyPleated aligned web filter
US6858297B1 (en)2004-04-052005-02-223M Innovative Properties CompanyAligned fiber web
US20060246260A1 (en)*2004-04-052006-11-023M Innovative Properties CompanyPleated Aligned Web Filter
KR100783450B1 (en)*2004-09-172007-12-07라이펜호이저 게엠베하 운트 코. 카게 마쉬넨파브릭Device for producing filaments from thermoplastic synthetic
US20060061006A1 (en)*2004-09-172006-03-23Reifenhaeuser Gmbh & Co. Kg MaschinenfabrikDevice for producing filaments from thermoplastic synthetic
CN1757800B (en)*2004-09-172010-05-05赖芬豪泽机械工厂有限及两合有限公司Device for producing filaments from thermoplastic synthetic
EP1637632A1 (en)*2004-09-172006-03-22Reifenhäuser GmbH & Co. MaschinenfabrikDevice for producing filaments from thermoplastic material
WO2006127578A1 (en)2005-05-232006-11-303M Innovative Properties CompanyMethods and apparatus for meltblowing of polymeric material utilizing fluid flow from an auxiliary manifold
US7698116B2 (en)2005-05-232010-04-133M Innovative Properties CompanyManifolds for delivering fluids having a desired mass flow profile and methods for designing the same
US20060265169A1 (en)*2005-05-232006-11-23Breister James CManifolds for delivering fluids having a desired mass flow profile and methods for designing the same
CN101184872B (en)*2005-05-232011-10-053M创新有限公司Methods and apparatus for meltblowing of polymeric material utilizing fluid flow from an auxiliary manifold
US7901614B2 (en)2005-05-232011-03-083M Innovative Properties CompanyMethods and apparatus for meltblowing of polymeric material utilizing fluid flow from an auxiliary manifold
US20060261525A1 (en)*2005-05-232006-11-23Breister James CMethods and apparatus for meltblowing of polymeric material utilizing fluid flow from an auxiliary manifold
US20090100937A1 (en)*2005-06-212009-04-23Unger Marketing International, Llc.Method of grading microfiber cleaning cloths
US20060283259A1 (en)*2005-06-212006-12-21Unger Marketing International, LlcMethod of grading microfiber cleaning cloths
US20080026688A1 (en)*2006-07-252008-01-31Paul MusickMethod and system for maintaining computer and data rooms
US8802002B2 (en)2006-12-282014-08-123M Innovative Properties CompanyDimensionally stable bonded nonwoven fibrous webs
US20080160861A1 (en)*2006-12-282008-07-03Berrigan Michael RDimensionally stable bonded nonwoven fibrous webs
US8608817B2 (en)2007-11-092013-12-17Hollingsworth & Vose CompanyMeltblown filter medium
US8986432B2 (en)2007-11-092015-03-24Hollingsworth & Vose CompanyMeltblown filter medium, related applications and uses
US20110147976A1 (en)*2007-11-092011-06-23Hollingsworth & Vose CompanyMeltblown filter medium
US10682595B2 (en)2009-04-032020-06-16Hollingsworth & Vose CompanyFilter media suitable for hydraulic applications
US8950587B2 (en)2009-04-032015-02-10Hollingsworth & Vose CompanyFilter media suitable for hydraulic applications
US9950284B2 (en)2009-04-032018-04-24Hollingsworth & Vose CompanyFilter media suitable for hydraulic applications
US20110037194A1 (en)*2009-08-142011-02-17Michael David JamesDie assembly and method of using same
WO2011019982A1 (en)*2009-08-142011-02-17The Procter & Gamble CompanySpinning die assembly and method for forming fibres using said assembly
US11414787B2 (en)2009-08-142022-08-16The Procter & Gamble CompanyDie assembly and methods of using same
US11739444B2 (en)2009-08-142023-08-29The Procter & Gamble CompanyDie assembly and methods of using same
US10704166B2 (en)2009-08-142020-07-07The Procter & Gamble CompanyDie assembly and method of using same
US20110220126A1 (en)*2010-03-112011-09-15Lebrette LaurentBiodegradable medical material
WO2011111028A1 (en)2010-03-112011-09-15Arjowiggins Palalda SasBiodegradable medical material
US10155187B2 (en)2010-04-272018-12-18Hollingsworth & Vose CompanyFilter media with a multi-layer structure
US8679218B2 (en)2010-04-272014-03-25Hollingsworth & Vose CompanyFilter media with a multi-layer structure
US9283501B2 (en)2010-04-272016-03-15Hollingsworth & Vose CompanyFilter media with a multi-layer structure
US10874962B2 (en)2010-12-172020-12-29Hollingsworth & Vose CompanyFine fiber filter media and processes
US10653986B2 (en)2010-12-172020-05-19Hollingsworth & Vose CompanyFine fiber filter media and processes
US10155186B2 (en)2010-12-172018-12-18Hollingsworth & Vose CompanyFine fiber filter media and processes
US11458427B2 (en)2010-12-172022-10-04Hollingsworth & Vose CompanyFine fiber filter media and processes
US9073061B2 (en)2011-12-022015-07-07W. L. Gore & Associates, Inc.Heat stabilized composite filter media and method of making the filter media
WO2013082381A1 (en)2011-12-022013-06-06W. L. Gore & Associates, Inc.Heat-stabilized composite filter media and method of making the filter media
US20150027380A1 (en)*2011-12-212015-01-29Unicharm CorporationPet sheet
AU2012354825B2 (en)*2011-12-212017-08-31Uni-Charm CorporationPet sheet
US20150150212A1 (en)*2012-07-062015-06-04Uni-Charm CorporationSheet for pets
US9694306B2 (en)2013-05-242017-07-04Hollingsworth & Vose CompanyFilter media including polymer compositions and blends
EP2918709A1 (en)2014-03-132015-09-16Fiber Innovation Technology, Inc.Multicomponent Aliphatic Polyester Fibers
WO2015164447A2 (en)2014-04-222015-10-29Fiber Innovation Technology, Inc.Fibers comprising an aliphatic polyester blend, and yarns, tows, and fabrics formed therefrom
US11019840B2 (en)2014-07-022021-06-01R.J. Reynolds Tobacco CompanyOral pouch products
US11793235B2 (en)2014-09-122023-10-24R.J. Reynolds Tobacco CompanyNonwoven pouch comprising heat sealable binder fiber
US10959456B2 (en)2014-09-122021-03-30R.J. Reynolds Tobacco CompanyNonwoven pouch comprising heat sealable binder fiber
US11832640B2 (en)2014-12-052023-12-05R.J. Reynolds Tobacco CompanyCapsule-containing pouched product for oral use
US10343095B2 (en)2014-12-192019-07-09Hollingsworth & Vose CompanyFilter media comprising a pre-filter layer
US12274968B2 (en)2014-12-192025-04-15Hollingsworth & Vose CompanyFilter media comprising a pre-filter layer
US12011686B2 (en)2014-12-192024-06-18Hollingsworth & Vose CompanyFilter media comprising a pre-filter layer
US11684885B2 (en)2014-12-192023-06-27Hollingsworth & Vose CompanyFilter media comprising a pre-filter layer
US11167232B2 (en)2014-12-192021-11-09Hollingsworth & Vose CompanyFilter media comprising a pre-filter layer
US11447893B2 (en)2017-11-222022-09-20Extrusion Group, LLCMeltblown die tip assembly and method
CN108589044A (en)*2018-06-262018-09-28桐乡守敬应用技术研究院有限公司A kind of melt-blow nonwoven processing unit (plant)
CN108691094A (en)*2018-06-262018-10-23桐乡守敬应用技术研究院有限公司A kind of melt-blow nonwoven processing unit (plant) that can uniformly mix staple fiber
WO2020020933A1 (en)*2018-07-272020-01-30Oerlikon Textile Gmbh & Co. KgMelt-spinning device for extruding very fine polymer particles
US11787152B2 (en)2018-12-132023-10-17North Carolina State UniversityMethod of preparing a composite sheet
US12138342B2 (en)2019-12-092024-11-12Nicoventures Trading LimitedFleece for oral product with releasable component
WO2021116852A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedOral product with dissolvable component
WO2021116881A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedOral product in a pourous pouch comprising a fleece material
US12178905B2 (en)2019-12-092024-12-31Nicoventures Trading LimitedFleece for pouched product with controlled basis weight
WO2021116884A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedLayered fleece for pouched product
WO2021116919A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedFleece for oral product with releasable component
WO2021116894A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedPouched products with heat sealable binder
EP4549642A2 (en)2019-12-092025-05-07Nicoventures Trading LimitedFleece for oral product with releasable component
WO2021116853A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedFibrous fleece material
WO2021116917A1 (en)2019-12-092021-06-17Nicoventures Trading LimitedOral composition with nanocrystalline cellulose
CN112176435A (en)*2020-10-142021-01-05安徽伯辉智能装备有限公司Melt cooling device for melt-blown non-woven fabric production
WO2022162558A1 (en)2021-01-282022-08-04Nicoventures Trading LimitedMethod for sealing pouches
WO2022224196A1 (en)2021-04-222022-10-27Nicoventures Trading LimitedOrally dissolving films
WO2022229926A1 (en)2021-04-302022-11-03Nicoventures Trading LimitedMulti-compartment oral pouched product
WO2023084498A1 (en)2021-11-152023-05-19Nicoventures Trading LimitedOral products with nicotine-polymer complex
WO2023084499A1 (en)2021-11-152023-05-19Nicoventures Trading LimitedProducts with enhanced sensory characteristics
WO2023194959A1 (en)2022-04-062023-10-12Nicoventures Trading LimitedPouched products with heat sealable binder
WO2024079722A1 (en)2022-10-142024-04-18Nicoventures Trading LimitedCapsule-containing pouched products
WO2024089588A1 (en)2022-10-242024-05-02Nicoventures Trading LimitedShaped pouched products
WO2024095164A1 (en)2022-11-012024-05-10Nicoventures Trading LimitedProducts with spherical filler
WO2024180481A1 (en)2023-02-282024-09-06Nicoventures Trading LimitedCaffeine-containing oral product
EP4599698A1 (en)2024-02-072025-08-13Nicoventures Trading LimitedProducts comprising sensory agents
WO2025169122A1 (en)2024-02-072025-08-14Nicoventures Trading LimitedProducts comprising sensory agents

Also Published As

Publication numberPublication date
AU592811B2 (en)1990-01-25
NZ216982A (en)1990-01-29
DE3687053T2 (en)1993-05-27
EP0212540B1 (en)1992-11-04
EP0212540A2 (en)1987-03-04
ZA865951B (en)1988-03-30
DE3687053D1 (en)1992-12-10
ES2001071A6 (en)1988-04-16
US4908163A (en)1990-03-13
EP0212540A3 (en)1989-09-27
JPS6245763A (en)1987-02-27
JPH0215656B2 (en)1990-04-12
AU6094186A (en)1987-02-12
BR8603783A (en)1987-03-17
CA1318993C (en)1993-06-15

Similar Documents

PublicationPublication DateTitle
US4622259A (en)Nonwoven medical fabric
EP0218473B1 (en)Nonwoven fabric with improved abrasion resistance
US4774125A (en)Nonwoven fabric with improved abrasion resistance
US5766737A (en)Nonwoven fabrics having differential aesthetic properties and processes for producing the same
EP0722389B1 (en)Controlled-porosity, calendered spunbonded/melt blown laminates
EP0904442B1 (en)Low or sub-denier nonwoven fibrous structures
AU660890B2 (en)Composite nonwoven fabrics and method of making same
CA1152879A (en)Nonwoven fabric of netting and thermoplastic microfibers
EP0421649B1 (en)Self-bonded fibrous nonwoven webs
US6723669B1 (en)Fine multicomponent fiber webs and laminates thereof
US5176952A (en)Modulus nonwoven webs based on multi-layer blown microfibers
EP0754796B1 (en)Nonwoven laminate fabrics and processes of making same
US5073436A (en)Multi-layer composite nonwoven fabrics
WO2000037723A2 (en)Fine multicomponent fiber webs and laminates thereof
EP0833002B1 (en)Flexible nonwoven fabric and laminate thereof
US20040152387A1 (en)Nonwoven fibrous sheet structures
US20030129910A1 (en)Multiple-layered nonwoven constructs for improved barrier performance

Legal Events

DateCodeTitleDescription
ASAssignment

Owner name:SURGIKOS, INC., A CORP OF NEW JERSEY

Free format text:ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:MC AMISH, LARRY H.;ADDY, TRALANCE O.;LEE, GEORGE F.;REEL/FRAME:004442/0526;SIGNING DATES FROM 19850803 TO 19850805

STCFInformation on status: patent grant

Free format text:PATENTED CASE

FEPPFee payment procedure

Free format text:PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

ASAssignment

Owner name:JOHNSON & JOHNSON MEDICAL, INC., A NJ CORP., NEW J

Free format text:MERGER;ASSIGNORS:JOHNSON & JOHNSON PATIENT CARE, INC.;STERILE DESIGN, INC., (MERGED INTO);SURGIKOS, INC. (CHANGED TO);REEL/FRAME:005315/0630

Effective date:19891204

FPAYFee payment

Year of fee payment:4

FPAYFee payment

Year of fee payment:8

ASAssignment

Owner name:CHICOPEE, INC., SOUTH CAROLINA

Free format text:ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:JOHNSON & JOHNSON MEDICAL, INC.;REEL/FRAME:007434/0483

Effective date:19950308

ASAssignment

Owner name:CHASE MANHATTAN BANK, THE, (N.A.), NEW YORK

Free format text:SECURITY INTEREST;ASSIGNOR:CHICOPEE, INC.;REEL/FRAME:007428/0344

Effective date:19940315

ASAssignment

Owner name:CHASE MANHATTAN BANK, THE, (THE), NEW YORK

Free format text:CORRECTIV;ASSIGNOR:CHICOPEE, INC.;REEL/FRAME:007881/0605

Effective date:19950315

ASAssignment

Owner name:CHASE MANHATTAN BANK (NATIONAL ASSOCIATION), NEW Y

Free format text:SECURITY INTEREST;ASSIGNORS:POLYMER GROUP, INC.;CHICOPEE, INC.;FIBERTECH GROUP, INC.;REEL/FRAME:008376/0030

Effective date:19960515

ASAssignment

Owner name:CHASE MANHATTAN BANK, THE, NEW YORK

Free format text:SECURITY INTEREST;ASSIGNOR:CHICOPEE, INC.;REEL/FRAME:008744/0462

Effective date:19970703

FEPPFee payment procedure

Free format text:PAYER NUMBER DE-ASSIGNED (ORIGINAL EVENT CODE: RMPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

Free format text:PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

FPAYFee payment

Year of fee payment:12

ASAssignment

Owner name:JPMORGAN CHASE BANK, NEW YORK

Free format text:SECURITY AGREEMENT;ASSIGNOR:CHICOPEE, INC.;REEL/FRAME:014186/0124

Effective date:20030305

ASAssignment

Owner name:CHICOPEE, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST;ASSIGNOR:JPMORGAN CHASE BANK, AS ADMINISTRATIVE AGENT;REEL/FRAME:016059/0415

Effective date:20040427

ASAssignment

Owner name:CITICORP NORTH AMERICA, INC. AS FIRST LIEN COLLATE

Free format text:SECURITY AGREEMENT;ASSIGNORS:CHICOPEE, INC.;FIBERTECH GROUP, INC;POLY-BOND, INC.;AND OTHERS;REEL/FRAME:015732/0080

Effective date:20040805

ASAssignment

Owner name:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERA

Free format text:SECURITY AGREEMENT;ASSIGNORS:CHICOPEE, INC.;FIBERTECH GROUP, INC.;POLY-BOND, INC.;AND OTHERS;REEL/FRAME:015778/0311

Effective date:20040805

ASAssignment

Owner name:PGI EUROPE, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:FNA ACQUISITION, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:FNA POLYMER CORP., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:FABRENE CORP., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:PRISTINE BRANDS CORPORATION, SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:FIBERGOL CORPORATION, SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:FABRENE GROUP L.L.C., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:POLYLONIX SEPARATION TECHNOLOGIES, INC., SOUTH CAR

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:LORETEX CORPORATION, SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:PNA CORPORATION, SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:FABRENE GROUP L.L.C., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:PGI POLYMER, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:PNA CORPORATION, SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:FNA ACQUISITION, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:FABRENE CORP., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:FNA POLYMER CORP., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:CHICOPEE, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:POLYLONIX SEPARATION TECHNOLOGIES, INC., SOUTH CAR

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:POLY-BOND INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:DOMINION TEXTILE (USA) INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:DOMINION TEXTILE (USA) INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:PGI EUROPE, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:FIBERGOL CORPORATION, SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:LORETEX CORPORATION, SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:BONLAM (S.C.), INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:POLY-BOND INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:FIBERTECH GROUP, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:BONLAM (S.C.), INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:TECHNETICS GROUP, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:POLYMER GROUP, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:TECHNETICS GROUP, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:FABPRO ORIENTED POLYMERS, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:PGI POLYMER, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:FABPRO ORIENTED POLYMERS, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:FIBERTECH GROUP, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:CHICOPEE, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:CITICORP NORTH AMERICA, INC., AS FIRST LIEN COLLATERAL AGENT;REEL/FRAME:016851/0436

Effective date:20051122

Owner name:POLYMER GROUP, INC., SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122

Owner name:PRISTINE BRANDS CORPORATION, SOUTH CAROLINA

Free format text:RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:WILMINGTON TRUST COMPANY, AS SECOND LIEN COLLATERAL AGENT;REEL/FRAME:016851/0471

Effective date:20051122


[8]ページ先頭

©2009-2025 Movatter.jp